JP3785009B2 - Continuous heating furnace for activation treatment - Google Patents

Continuous heating furnace for activation treatment Download PDF

Info

Publication number
JP3785009B2
JP3785009B2 JP33723799A JP33723799A JP3785009B2 JP 3785009 B2 JP3785009 B2 JP 3785009B2 JP 33723799 A JP33723799 A JP 33723799A JP 33723799 A JP33723799 A JP 33723799A JP 3785009 B2 JP3785009 B2 JP 3785009B2
Authority
JP
Japan
Prior art keywords
chamber
purge
heating
gas
purge chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP33723799A
Other languages
Japanese (ja)
Other versions
JP2001158612A (en
Inventor
正勝 柳田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Koyo Thermo Systems Co Ltd
Original Assignee
Koyo Thermo Systems Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Koyo Thermo Systems Co Ltd filed Critical Koyo Thermo Systems Co Ltd
Priority to JP33723799A priority Critical patent/JP3785009B2/en
Publication of JP2001158612A publication Critical patent/JP2001158612A/en
Application granted granted Critical
Publication of JP3785009B2 publication Critical patent/JP3785009B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Carbon And Carbon Compounds (AREA)
  • Tunnel Furnaces (AREA)
  • Furnace Details (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、揮発性物質を含む炭素質材料からなる被処理物を、水蒸気雰囲気中で加熱する賦活処理用連続加熱炉に関する。
【0002】
【従来の技術】
この種の連続加熱炉として、被処理物を搬送装置により入口パージ室を通して加熱室に搬入し、この加熱室にて水蒸気雰囲気中で500〜1000℃に加熱処理して揮発性物質を蒸散させた後、前記搬送装置により冷却室に移送して冷却し、出口パージ室を通して炉外に搬出するものが知られている。
かかる賦活処理用連続加熱炉においては、炭素質材料に含まれているタールやピッチ等の揮発性物質から揮発成分が炉内に排出されるが、この排出された揮発物質は、炉外に導かれて燃焼廃棄されている。
【0003】
【発明が解決しようとする課題】
前記従来の賦活処理用連続加熱炉は、その使用中において前記入口パージ室及び出口パージ室に、窒素ガス等のパージガスを常時供給する必要がある。このため、多量のパージガスを消費し、処理コストが高く付くという問題があった。また、被処理物から揮発した物質を燃焼した際に発生するガスをそのまま大気に放出すると環境負荷となるという問題もあった。
【0004】
上記のような従来の問題点に鑑み、この発明は、パージ室に供給している従来のパージガスを不要にすることができるとともに、揮発した物質の燃焼により発生するガスをパージガスとして循環再利用することにより、環境負荷の低減を図ることができる賦活処理用連続加熱炉を提供することを目的とする。
【0005】
【課題を解決するための手段】
前記目的を達成するためのこの発明の賦活処理用連続加熱炉は、揮発性物質を含む炭素質材料からなる被処理物を水蒸気雰囲気中で加熱する加熱室と、この加熱室で加熱した被処理物を冷却する冷却室と、前記加熱室の被処理物の搬入側に設けられた入口パージ室と、前記冷却室の被処理物の搬出側に設けられた出口パージ室と、被処理物を前記入口パージ室、加熱室、冷却室及び出口パージ室に順次搬送する搬送装置とを備える賦活処理用連続加熱炉において、前記被処理物から揮発した物質を加熱室から炉外に回収する回収装置と、回収した揮発物質を燃焼させる燃焼装置と、燃焼装置で発生するガスを入口パージ室及び出口パージ室に供給するガス供給装置とを備え、前記燃焼装置で発生するガスを直接大気に廃棄することなくパージガスとして循環再利用することを特徴とする。
このように構成された賦活処理用連続加熱炉は、加熱室において被処理物から揮発した物質を、前記回収装置によって回収し、この回収した揮発物質を燃焼装置によって燃焼させ、当該燃焼装置で発生するガスを、ガス供給装置によってパージガスとして入口パージ室及び出口パージ室に供給することができ、これにより、前記燃焼装置で発生するガスを直接大気に廃棄することなくパージガスとして循環再利用することができる。
【0006】
【発明の実施の形態】
図1は、この発明の賦活処理用連続加熱炉の一実施形態を示す模式図である。この連続加熱炉は、揮発性物質を含む被処理物を加熱及び冷却する炉体1と、この炉体1の内部を挿通するネットコンベアからなる搬送装置2と、被処理物から揮発した物質(以下「揮発物質」という)を炉内から炉外に導いて回収する回収装置3と、回収した揮発物質を燃焼させる燃焼装置4と、この揮発物質の燃焼に伴って発生するのガスをパージガスとして燃焼装置4から炉体1に供給するガス供給装置5とにより主要部が構成されている。
【0007】
図2も参照して、前記炉体1は、被処理物を加熱する加熱室11と、この加熱室11で加熱した被処理物を冷却する冷却室12と、前記加熱室11に隣接させて被処理物の搬入側に設けられた入口パージ室13と、前記冷却室12に隣接させて被処理物の搬出側に設けられた出口パージ室14とを備えている。
【0008】
前記加熱室11は、搬送装置2によって入口パージ室13から搬入された被処理物を、水蒸気雰囲気中で500〜1000℃に加熱して賦活処理するものである。この加熱室11の周囲は断熱壁11aによって覆われており、搬送装置2の搬送面を挟んだ上下位置には、多数の噴射ノズルを有する蒸気配管11bが配列されている。また、前記加熱室11の入口パージ室13寄りの天井部には、雰囲気回収口11cが設けられており、加熱室11と入口パージ室13との境界部、及び加熱室11と冷却室12との境界部には、搬送装置2とその上に載置された被処理物の通過を許容した状態で仕切壁11dが設けられている。
【0009】
冷却室12は、加熱室11に続く徐冷域12aと、それに続く二重構造による外部水冷域12bから構成されており、この外部水冷域12bには、搬送空間を包囲した状態で水冷ジャッケト12cが配置されており、この水冷ジャッケト12cに炉外から冷却水を循環供給することにより、加熱室11から搬入された被処理物を冷却できるようになっている。
また、冷却室12と出口パージ室14との境界部には、搬送装置2とその上に載置された被処理物の通過を許容した状態で仕切壁12dが設けられている。
【0010】
入口パージ室13は、加熱室11の雰囲気をシールするためのものであり、その内部には前記燃焼装置4で発生するガスが、ガス供給装置5を介して供給されている。また、入口パージ室13の被処理物の搬入側には、搬送装置2とその上に載置された被処理物の通過を許容する開口13aが設けられており、その天井部には雰囲気回収口13bが設けられている。
出口パージ室14は、冷却室12の雰囲気をシールするためのものであり、その内部には前記燃焼装置4で発生するガスがガス供給装置5を介して供給されている。また、出口パージ室14の被処理物の搬出側には、搬送装置2とその上に載置された被処理物の通過を許容する開口14aが設けられており、その天井部には雰囲気回収口14bが設けられている。
【0011】
搬送装置2は、その搬送面側が前記炉体1を挿通した状態で無端回動するものであり、被処理物を入口パージ室13から出口パージ室14に向かって連続的に搬送する。
回収装置3は、加熱室11、入口パージ室13及び出口パージ室14のそれぞれの雰囲気回収口11c,13b,14bと燃焼装置4の燃焼室41とを配管31によって連通し、この配管31の途中部に、一対のトラップ32,33及び吸気ブロワー34を介在したものである。各トラップ32,33は水冷されており、一方のトラップ32は加熱室11及び入口パージ室13から排出される雰囲気ガス中に含まれるタールや水分を補捉し、他方のトラップ32は出口パージ室14から排出される雰囲気ガス中に含まれるタールや水分を補捉する。
【0012】
燃焼装置4は、前記回収装置3によって燃焼室41に回収された揮発物質を、バーナ42によって燃焼させるものであり、この燃焼に伴って二酸化炭素、窒素及び水蒸気を含むガスが発生し、当該ガスは燃焼室41の天井部に設けた取出し口43を通してガス供給装置5に導かれる。
【0013】
ガス供給装置5は、燃焼装置4の取出し口43と炉体1の各パージ室13,14とを配管51によって連通し、この配管51の途中部に、給気ブロワー52、流量調整弁53,54、及び流量計55,56を介在したものである。
このガス供給装置5は、燃焼装置4から例えば40m/Hrの流量を吸引し、流量調整弁53,54によって入口パージ室13に10m/Hr、出口パージ室14に30m/Hrの流量でパージガスとしてそのまま分配供給する。
【0014】
このように、前記連続加熱炉は、被処理物から排出された揮発物質の燃焼によって生じるガスを、入口パージ室13及び出口パージ室14に還流するので、このガスをパージガスとして再利用することができる。このため、従来供給していたパージガスが不要となり、その分賦活処理コストを削減することができる。また、燃焼装置4で発生するガスを直接大気に廃棄することなく循環再利用するので、環境負荷を低減することもできる。
この発明の連続加熱炉は、前記の実施の形態に限定されるものでなく、例えば、搬送装置2として前記ネットコンベアに代えてローラコンベアやプッシャーを使用すること等、種々の設計変更を施すことができる。
【0015】
【発明の効果】
以上のように、この発明の賦活処理用連続加熱炉によれば、被処理物から揮発した物質を燃焼して得られるガスを、入口パージ室及び出口パージ室に供給して、パージガスとして循環再利用することができるので、パージ室に供給している従来のパージガスが不要となり、その分、賦活処理費コストを低減することができる。また、燃焼装置で発生するガスを直接大気に廃棄することなく循環再利用するので、環境負荷を低減することもできる。
【図面の簡単な説明】
【図1】この発明の連続加熱炉の一実施形態を示す模式図である。
【図2】上記連続加熱炉の内部構成を示す断面図である。
【符号の説明】
1 炉体
11 加熱室
12 冷却室
13 入口パージ室
14 出口パージ室
2 搬送装置
3 回収装置
4 燃焼装置
5 ガス供給装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a continuous heating furnace for activation treatment in which an object to be processed made of a carbonaceous material containing a volatile substance is heated in a steam atmosphere.
[0002]
[Prior art]
As this type of continuous heating furnace, the object to be processed is carried into a heating chamber through an inlet purge chamber by a transfer device, and volatile substances are evaporated by heat treatment in a steam atmosphere at 500 to 1000 ° C. After that, there is known one that is transferred to a cooling chamber by the transfer device, cooled, and carried out of the furnace through an outlet purge chamber.
In such a continuous heating furnace for activation treatment, volatile components are discharged into the furnace from volatile substances such as tar and pitch contained in the carbonaceous material, and the discharged volatile substances are introduced outside the furnace. It is burned and discarded.
[0003]
[Problems to be solved by the invention]
The conventional continuous heating furnace for activation treatment needs to always supply a purge gas such as nitrogen gas to the inlet purge chamber and the outlet purge chamber during use. For this reason, there is a problem that a large amount of purge gas is consumed and the processing cost is high. In addition, there is a problem in that if the gas generated when the material volatilized from the object to be burned is released to the atmosphere as it is, it becomes an environmental burden.
[0004]
In view of the conventional problems as described above, the present invention can eliminate the need for the conventional purge gas supplied to the purge chamber, and circulate and reuse the gas generated by the combustion of the volatilized substance as the purge gas. Accordingly, an object of the present invention is to provide a continuous heating furnace for activation treatment that can reduce the environmental load.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, the continuous heating furnace for activation treatment according to the present invention includes a heating chamber for heating an object to be processed made of a carbonaceous material containing a volatile substance in a steam atmosphere, and an object to be processed heated in the heating chamber. A cooling chamber for cooling the object, an inlet purge chamber provided on the workpiece carry-in side of the heating chamber, an outlet purge chamber provided on the workpiece discharge side of the cooling chamber, and the workpiece In the continuous heating furnace for activation treatment, comprising a transfer device that sequentially transfers to the inlet purge chamber, heating chamber, cooling chamber, and outlet purge chamber, a recovery device that recovers the material volatilized from the workpiece from the heating chamber to the outside of the furnace And a combustion device for combusting the recovered volatile substances, and a gas supply device for supplying the gas generated in the combustion device to the inlet purge chamber and the outlet purge chamber, and directly discarding the gas generated in the combustion device to the atmosphere Purge without And wherein the circulating re-use as a nest.
The continuous heating furnace for activation treatment configured in this way recovers the material volatilized from the object to be processed in the heating chamber by the recovery device, burns the recovered volatile material by the combustion device, and generates it in the combustion device. The gas to be supplied can be supplied to the inlet purge chamber and the outlet purge chamber as a purge gas by the gas supply device, so that the gas generated in the combustion device can be circulated and reused as the purge gas without being directly discarded to the atmosphere. it can.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a schematic diagram showing an embodiment of a continuous heating furnace for activation treatment according to the present invention. This continuous heating furnace includes a furnace body 1 that heats and cools an object to be processed containing a volatile substance, a transfer device 2 that includes a net conveyor that passes through the inside of the furnace body 1, and a substance ( (Hereinafter referred to as “volatile substances”) from the furnace to the outside of the furnace for recovery, a recovery apparatus 3 for combusting the recovered volatile substances, and a gas generated by the combustion of the volatile substances as a purge gas A main part is constituted by the gas supply device 5 supplied from the combustion device 4 to the furnace body 1.
[0007]
Referring also to FIG. 2, the furnace body 1 is adjacent to the heating chamber 11 for heating the workpiece, the cooling chamber 12 for cooling the workpiece heated in the heating chamber 11, and the heating chamber 11. An inlet purge chamber 13 provided on the workpiece carry-in side and an outlet purge chamber 14 provided on the workpiece carry-out side adjacent to the cooling chamber 12 are provided.
[0008]
The heating chamber 11 heats the workpiece carried from the inlet purge chamber 13 by the transport device 2 to a temperature of 500 to 1000 ° C. in a steam atmosphere, and activates the workpiece. The periphery of the heating chamber 11 is covered with a heat insulating wall 11a, and steam pipes 11b having a large number of injection nozzles are arranged at upper and lower positions sandwiching the transport surface of the transport device 2. In addition, an atmosphere recovery port 11c is provided in the ceiling portion of the heating chamber 11 near the inlet purge chamber 13, and the boundary between the heating chamber 11 and the inlet purge chamber 13, and the heating chamber 11 and the cooling chamber 12, A partition wall 11d is provided at a boundary portion of the transfer device 2 in a state in which the transfer device 2 and the workpiece placed thereon are allowed to pass.
[0009]
The cooling chamber 12 is composed of a slow cooling region 12a following the heating chamber 11, and an external water cooling region 12b having a double structure following the heating chamber 11, and a water cooling jacket 12c is disposed in the external water cooling region 12b so as to surround the conveyance space. In addition, by circulating and supplying cooling water from the outside of the furnace to the water-cooled jacket 12c, it is possible to cool the workpiece carried in from the heating chamber 11.
In addition, a partition wall 12d is provided at the boundary between the cooling chamber 12 and the outlet purge chamber 14 in a state in which passage of the transfer device 2 and an object to be processed placed thereon is permitted.
[0010]
The inlet purge chamber 13 is for sealing the atmosphere of the heating chamber 11, and the gas generated in the combustion device 4 is supplied to the inside via the gas supply device 5. Further, on the carry-in side of the workpiece in the inlet purge chamber 13, an opening 13a that allows passage of the workpiece 2 and the workpiece placed thereon is provided, and an atmosphere recovery is provided on the ceiling portion. A mouth 13b is provided.
The outlet purge chamber 14 is for sealing the atmosphere of the cooling chamber 12, and the gas generated in the combustion device 4 is supplied to the inside through the gas supply device 5. In addition, on the side of the outlet purge chamber 14 where the object to be processed is carried out, there is provided an opening 14a that allows the conveying device 2 and the object to be processed placed thereon to pass through, and an atmosphere recovery is provided on the ceiling. A mouth 14b is provided.
[0011]
The transfer device 2 rotates endlessly with the transfer surface side inserted through the furnace body 1, and continuously transfers the object to be processed from the inlet purge chamber 13 toward the outlet purge chamber 14.
The recovery device 3 communicates the atmosphere recovery ports 11 c, 13 b, 14 b of the heating chamber 11, the inlet purge chamber 13 and the outlet purge chamber 14 with the combustion chamber 41 of the combustion device 4 through a pipe 31. A pair of traps 32 and 33 and an intake blower 34 are interposed in the section. The traps 32 and 33 are water-cooled, one trap 32 captures tar and moisture contained in the atmospheric gas discharged from the heating chamber 11 and the inlet purge chamber 13, and the other trap 32 is the outlet purge chamber. 14 captures the tar and moisture contained in the atmospheric gas discharged from 14.
[0012]
The combustion device 4 burns the volatile substance recovered in the combustion chamber 41 by the recovery device 3 by the burner 42, and a gas containing carbon dioxide, nitrogen and water vapor is generated along with the combustion, and the gas Is guided to the gas supply device 5 through an outlet 43 provided in the ceiling of the combustion chamber 41.
[0013]
The gas supply device 5 communicates the take-out port 43 of the combustion device 4 and the purge chambers 13, 14 of the furnace body 1 by a pipe 51, and an air supply blower 52, a flow rate adjustment valve 53, 54 and flow meters 55 and 56 are interposed.
The gas supply device 5, the flow rate of the combustion device 4, for example 40 m 3 / Hr with suction, 10 m 3 / Hr to the inlet purge chamber 13 by the flow control valve 53, a flow rate of 30 m 3 / Hr into the outlet purge chamber 14 Then, it is distributed and supplied as a purge gas.
[0014]
As described above, the continuous heating furnace recirculates the gas generated by the combustion of the volatile matter discharged from the workpiece to the inlet purge chamber 13 and the outlet purge chamber 14, so that this gas can be reused as the purge gas. it can. For this reason, the purge gas supplied conventionally becomes unnecessary and the activation processing cost can be reduced. Further, since the gas generated in the combustion device 4 is recycled and reused without being directly discarded into the atmosphere, the environmental load can be reduced.
The continuous heating furnace of the present invention is not limited to the above-described embodiment, and various design changes such as using a roller conveyor or a pusher instead of the net conveyor as the transfer device 2 are performed. Can do.
[0015]
【The invention's effect】
As described above, according to the continuous heating furnace for activation treatment of the present invention, the gas obtained by burning the material volatilized from the workpiece is supplied to the inlet purge chamber and the outlet purge chamber, and circulated again as the purge gas. Since it can be utilized, the conventional purge gas supplied to the purge chamber becomes unnecessary, and the activation processing cost can be reduced correspondingly. In addition, since the gas generated in the combustion apparatus is recycled and reused without being directly discarded into the atmosphere, the environmental load can be reduced.
[Brief description of the drawings]
FIG. 1 is a schematic view showing an embodiment of a continuous heating furnace according to the present invention.
FIG. 2 is a cross-sectional view showing an internal configuration of the continuous heating furnace.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Furnace 11 Heating chamber 12 Cooling chamber 13 Inlet purge chamber 14 Outlet purge chamber 2 Conveying device 3 Recovery device 4 Combustion device 5 Gas supply device

Claims (1)

揮発性物質を含む炭素質材料からなる被処理物を水蒸気雰囲気中で加熱する加熱室と、この加熱室で加熱した被処理物を冷却する冷却室と、前記加熱室の被処理物の搬入側に設けられた入口パージ室と、前記冷却室の被処理物の搬出側に設けられた出口パージ室と、被処理物を前記入口パージ室、加熱室、冷却室及び出口パージ室に順次搬送する搬送装置とを備える賦活処理用連続加熱炉において、
前記被処理物から揮発した物質を加熱室から炉外に回収する回収装置と、
回収した揮発物質を燃焼させる燃焼装置と、
燃焼装置で発生するガスを入口パージ室及び出口パージ室に供給するガス供給装置とを備え、
前記燃焼装置で発生するガスを直接大気に廃棄することなくパージガスとして循環再利用することを特徴とする賦活処理用連続加熱炉。
A heating chamber for heating an object to be processed made of a carbonaceous material containing a volatile substance in a water vapor atmosphere, a cooling chamber for cooling the object to be processed heated in the heating chamber, and a loading side of the object to be processed in the heating chamber The inlet purge chamber provided in the cooling chamber, the outlet purge chamber provided on the workpiece discharge side of the cooling chamber, and the workpiece are sequentially transferred to the inlet purge chamber, heating chamber, cooling chamber, and outlet purge chamber. In a continuous heating furnace for activation treatment comprising a transport device,
A recovery device for recovering a substance volatilized from the object to be processed from the heating chamber to the outside of the furnace;
A combustion device for burning the recovered volatile substances;
A gas supply device for supplying gas generated in the combustion device to the inlet purge chamber and the outlet purge chamber,
A continuous heating furnace for activation treatment, wherein the gas generated in the combustion device is recycled and reused as purge gas without being directly discarded into the atmosphere.
JP33723799A 1999-11-29 1999-11-29 Continuous heating furnace for activation treatment Expired - Fee Related JP3785009B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33723799A JP3785009B2 (en) 1999-11-29 1999-11-29 Continuous heating furnace for activation treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33723799A JP3785009B2 (en) 1999-11-29 1999-11-29 Continuous heating furnace for activation treatment

Publications (2)

Publication Number Publication Date
JP2001158612A JP2001158612A (en) 2001-06-12
JP3785009B2 true JP3785009B2 (en) 2006-06-14

Family

ID=18306743

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33723799A Expired - Fee Related JP3785009B2 (en) 1999-11-29 1999-11-29 Continuous heating furnace for activation treatment

Country Status (1)

Country Link
JP (1) JP3785009B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5571292B2 (en) * 2008-03-27 2014-08-13 光洋サーモシステム株式会社 Continuous firing furnace

Also Published As

Publication number Publication date
JP2001158612A (en) 2001-06-12

Similar Documents

Publication Publication Date Title
US4168951A (en) Method of sintering and apparatus for carrying out the method
US5098286A (en) Regenerative thermal incinerator apparatus
JP4393628B2 (en) Multi-stage rotary kiln
JP2001232342A (en) Cleaning apparatus for contaminated soil including volatile organic compound
KR100858888B1 (en) A method of processing organic material and a processing apparatus
JP3785009B2 (en) Continuous heating furnace for activation treatment
JP2005274017A (en) Drying and treating method, system, and facility for wet material
JP4020645B2 (en) Externally heated rotary kiln
JP5102499B2 (en) Rotary carbonization method and apparatus
JP3937232B2 (en) Carbonization equipment
JPH06147778A (en) Tunnel kiln for baking carbon product
JP4023582B2 (en) Grain drying equipment
JPH10238728A (en) Heat treatment facility for waste and method therefor
US4846678A (en) Means and method for heat treatment of green bodies
JP3617940B2 (en) Circulating dryer
JPH03207792A (en) Continuous wood carbonization device utilizing electric oven
JP3274092B2 (en) Heat treatment system
JP6452144B2 (en) Powder processing equipment
JPH0354135Y2 (en)
JPH06323738A (en) Roller hearth kiln
JPS58133315A (en) Thermostatic annealing apparatus
JP3744401B2 (en) Heat treatment method and heat treatment apparatus
JPH087275Y2 (en) Evaporative cleaning device for adhering oil on finned Al heat exchanger
JPS62112982A (en) Fiber calciner
JPS60137855A (en) Quick lime baking apparatus

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050627

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060221

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060316

R150 Certificate of patent or registration of utility model

Ref document number: 3785009

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120324

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120324

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130324

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130324

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140324

Year of fee payment: 8

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees